Classifications

• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L9/00—Compositions of homopolymers or copolymers of conjugated diene hydrocarbons
  • C08L9/06—Copolymers with styrene
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B60—VEHICLES IN GENERAL
  • B60C—VEHICLE TYRES; TYRE INFLATION; TYRE CHANGING; CONNECTING VALVES TO INFLATABLE ELASTIC BODIES IN GENERAL; DEVICES OR ARRANGEMENTS RELATED TO TYRES
  • B60C1/00—Tyres characterised by the chemical composition or the physical arrangement or mixture of the composition
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B60—VEHICLES IN GENERAL
  • B60C—VEHICLE TYRES; TYRE INFLATION; TYRE CHANGING; CONNECTING VALVES TO INFLATABLE ELASTIC BODIES IN GENERAL; DEVICES OR ARRANGEMENTS RELATED TO TYRES
  • B60C1/00—Tyres characterised by the chemical composition or the physical arrangement or mixture of the composition
  • B60C1/0016—Compositions of the tread
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J3/00—Processes of treating or compounding macromolecular substances
  • C08J3/20—Compounding polymers with additives, e.g. colouring
  • C08J3/205—Compounding polymers with additives, e.g. colouring in the presence of a continuous liquid phase
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J3/00—Processes of treating or compounding macromolecular substances
  • C08J3/20—Compounding polymers with additives, e.g. colouring
  • C08J3/22—Compounding polymers with additives, e.g. colouring using masterbatch techniques
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J3/00—Processes of treating or compounding macromolecular substances
  • C08J3/20—Compounding polymers with additives, e.g. colouring
  • C08J3/22—Compounding polymers with additives, e.g. colouring using masterbatch techniques
  • C08J3/226—Compounding polymers with additives, e.g. colouring using masterbatch techniques using a polymer as a carrier
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
  • C08K3/00—Use of inorganic substances as compounding ingredients
  • C08K3/02—Elements
  • C08K3/04—Carbon
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
  • C08K5/00—Use of organic ingredients
  • C08K5/36—Sulfur-, selenium-, or tellurium-containing compounds
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
  • C08K5/00—Use of organic ingredients
  • C08K5/36—Sulfur-, selenium-, or tellurium-containing compounds
  • C08K5/39—Thiocarbamic acids; Derivatives thereof, e.g. dithiocarbamates
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L21/00—Compositions of unspecified rubbers
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L9/00—Compositions of homopolymers or copolymers of conjugated diene hydrocarbons
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L9/00—Compositions of homopolymers or copolymers of conjugated diene hydrocarbons
  • C08L9/06—Copolymers with styrene
  • C08L9/08—Latex
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J2309/00—Characterised by the use of homopolymers or copolymers of conjugated diene hydrocarbons
  • C08J2309/06—Copolymers with styrene
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J2409/00—Characterised by the use of homopolymers or copolymers of conjugated diene hydrocarbons
  • C08J2409/06—Copolymers with styrene
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L2207/00—Properties characterising the ingredient of the composition
  • C08L2207/32—Properties characterising the ingredient of the composition containing low molecular weight liquid component
  • C08L2207/324—Liquid component is low molecular weight polymer

Definitions

• the present invention relates to a rubber composition for tire treads and a tire manufactured using the same. More particularly, a rubber composition for tire treads that may be applied to an ultra-high tire by exhibiting grip and anti-wear performances under a condition of heavy load, high slip and high speed, and a tire manufactured using the same.
• ultra-high performance tires require enhanced high grip force and anti-wear properties under a condition of heavy load, high slip and high speed.
• a reinforcing filler is included in a large amount in order to meet high vehicle performances of high-end vehicles, durability is enhanced but grip performance is decreased, thereby dramatically decreasing overall performances of a tire.
• Tg in order to increase Tg, a new polymer should be obtained, but, in the case of a special grade, it is not easy to obtain a new polymer.
• Tg is increased, lots of debris as in F1 Pirelli tire is remained on roads and wearing is rapidly progressed.
• EP 2610298 A1 describes a known method for manufacturing a rubber composition for tires.
• FR 2955588 A1 describes a known elastomeric composition for a tire.
• the present invention has been made in view of the above problems, and it is an object of the present invention to provide a rubber composition for tire treads that may be usefully applied to an ultra-high performance tire due to enhanced grip and anti-wear performances under a condition of heavy load, high slip and high speed.
• a rubber composition for tire treads including 50 to 200 parts by weight of a wet masterbatch prepared by mixing a styrene-butadiene latex, a carbon black and a liquid styrene-butadiene copolymer at 50 to 95°C for three to nine hours according to a batchwise method, 60 to 70 parts by weight of a raw rubber and 50 to 200 parts by weight of a carbon black.
• a terminal hydrogen of the liquid styrene-butadiene copolymer is substituted with any one selected from the group consisting of a C1 to C10 alkyl group, a C3 to C30 cycloalkyl group, a C2 to C30 heterocycloalkyl, a C3 to C30 aryl group and a C2 to C30 heteroaryl group.
• the wet masterbatch may be prepared by mixing 60 to 150 parts by weight of the carbon black and 60 to 200 parts by weight of the liquid styrene-butadiene copolymer with respect to 100 parts by weight of the styrene-butadiene latex.
• the amount of styrene may be 17 to 27 wt%, and the amount of vinyl in butadiene may be 60 to 80 wt%.
• the amount of styrene may be 40 to 60 wt%, and the amount of vinyl in butadiene may be 15 to 45 wt%.
• the carbon black may have an iodine absorption amount of 200 to 1000 mg/g and an N-dibutyl phthalate (DBP) oil absorption amount of 150 to 800 cc/100 g.
• DBP N-dibutyl phthalate
• the wet masterbatch may be prepared by further adding a processing oil in an amount of 10 to 100 parts by weight.
• the processing oil may include 35 ⁇ 5 wt% of an aromatic ingredient, 28 ⁇ 5 wt% of a naphthenic ingredient and 38 ⁇ 5 wt% of a paraffin based ingredient with respect to the total amount of the processing oil.
• the content of benzo(a)pyrene (BaP) as an ingredient among polycyclic aromatic hydrocarbon (PAH) may be 1 ppm or less, and a total content of eight PAH types such as benzo(a)pyrene (BaP), benzo(e)pyren (BeP), benzo(a)anthracene (BaA), chrysen (CHR), benzo(b)fluoranthene (BbFA), benzo(j)fluoranthene (BjFA), benzo(k)fluoranthene (BkFA) and dibenzo(a,h)anthracene may be 10 ppm or less.
• PAH polycyclic aromatic hydrocarbon
• the raw rubber may be a styrene-butadiene rubber in which the content of styrene is 30 to 50 wt%, the content of vinyl in butadiene is 40 to 65 wt%, the content of oil is 5 to 45 wt%, and glass transition temperature is -19°C to -29°C.
• a rubber composition for tire treads includes 1) 50 to 200 parts by weight of a wet masterbatch that is prepared by mixing styrene-butadiene latex, carbon black and a liquid styrene-butadiene copolymer, 2) 60 to 70 parts by weight of a raw rubber, and 3) 50 to 200 parts by weight of a carbon black.
• the wet masterbatch is prepared by reacting i) the styrene-butadiene latex, ii) the carbon black and iii) the liquid styrene-butadiene copolymer at 50 to 95°C for three to nine hours time according to a batchwise method.
• the wet masterbatch is reacted for three to nine hours at 50 to 95°C after inputting water into a batchwise reactor and inputting i) the styrene-butadiene latex, ii) the carbon black, and iii) the liquid styrene-butadiene copolymer into the reactor, according to a batchwise method.
• moisture is evaporated while stirring a reaction product, and the reaction product may be extruded into a sheet type by passing through a roll.
• reaction temperature when reaction temperature is less than 50°C upon preparation of the wet masterbatch, synthesis reaction between raw materials might not occur. When reaction temperature is greater than 95°C, water in the reactor is evaporated, and thus, dispersibility may be decreased. In addition, upon preparation of the wet masterbatch, synthesis reaction between raw materials might not occur when a reaction time is less than three hours, and, since additional reaction does not proceed when a reaction time exceeds nine hours, it is unnecessary to exceed nine hours.
• the wet masterbatch may be prepared by mixing i) 100 parts by weight of the styrene-butadiene latex, ii) 60 to 150 parts by weight of the carbon black, and iii) 60 to 200 parts by weight of the liquid styrene-butadiene copolymer.
• the content of carbon black is less than 60 parts by weight, improvement effects according to use of the carbon black are insignificant.
• the content of carbon black exceeds 150 parts by weight, dispersion time is reduced due to heating, and thus, dispersibility may be decreased.
• liquid styrene-butadiene copolymer when the content of liquid styrene-butadiene copolymer is less than 60 parts by weight, improvement effects according to use of the liquid styrene-butadiene copolymer is insignificant during reaction. When the content of liquid styrene-butadiene copolymer exceeds 200 parts by weight, processability may be deteriorated.
• a terminal hydrogen of the liquid styrene-butadiene copolymer is substituted with any one selected from the group consisting of a C1 to C10 alkyl group, a C3 to C30 cycloalkyl group, a C2 to C30 heterocycloalkyl group, a C3 to C30 aryl group and a C2 to C30 heteroaryl group, preferably a methyl group, an ethyl group, a cyclobutyl group, a cyclohexyl group, or a phenyl group.
• the wet masterbatch may use the liquid styrene-butadiene copolymer instead of a processing oil used in a wet masterbatch, or may include a small amount of iv) a processing oil. That is, the wet masterbatch may be prepared by further adding 10 to 100 parts by weight of the processing oil, preferably 10 to 45 parts by weight of the processing oil. In this case, dispersibility of the styrene-butadiene latex, the carbon black and the liquid styrene-butadiene copolymer may be further enhanced.
• an eco-friendly residual aromatic extract (RAE) oil in which the content of benzo(a)pyrene (BaP) as an ingredient among polycyclic aromatic hydrocarbon (PAH) is 1 ppm or less, and the total content of eight PAH types such as benzo(a)pyrene (BaP), benzo(e)pyren (BeP), benzo(a)anthracene (BaA), chrysen (CHR), benzo(b)fluoranthene (BbFA), benzo(j)fluoranthene (BjFA), benzo(k)fluoranthene (BkFA), dibenzo(a,h)anthracene is 10 ppm or less, may be preferably used.
• PAH polycyclic aromatic hydrocarbon
• the raw rubber include polyisoprene rubber, polybutadiene rubber, conjugated diene aromatic vinyl copolymers, nitrile conjugated diene copolymers, hydrogenated NBR, hydrogenated NBR, olefin rubber, ethylene-propylene rubber modified with maleic acid, butyl rubber, a copolymer of isobutylene and aromatic vinyl or a diene monomer, acrylic rubber, ionomers, halogenated rubber, chloroprene rubber, or mixtures of one material type or two or more material types thereof.
• the raw rubber may preferably include styrene-butadiene rubber.
• the styrene-butadiene rubber is rubber solution-polymerized according to a batchwise method.
• the content of styrene is 30 to 50 wt%
• the content of vinyl in butadiene is 40 to 65 wt%
• the content of oil is 5 to 45 wt%
• Tg is -19 to -29°C.
• the weight-average molecular weight of the styrene-butadiene rubber may preferably be 400,000 to 1000,000 g/mol, and a molecular weight distribution thereof may preferably be 1.1 or less.
• the oil may preferably include, particularly, 35 ⁇ 5 wt% of an aromatic ingredient, 28 ⁇ 5 wt% of a naphthenic ingredient, 38 ⁇ 5 wt% of a paraffin based ingredient with respect to the total weight of the processing oil.
• an eco-friendly residual aromatic extraction oil in which the content of benzo(a)pyrene (BaP) as an ingredient among polycyclic aromatic hydrocarbon (PAH) is 1 ppm or less, and the total content of eight PAH types such as benzo(a)pyrene (BaP), benzo(e)pyren (BeP), benzo (a)anthracene (BaA), chrysen (CHR), benzo(b)fluoranthene (BbFA), benzo(j)fluoranthene (BjFA), benzo(k)fluoranthene (BkFA), dibenzo(a,h)anthracene is 10 ppm or less, may be more preferable.
• PAH polycyclic aromatic hydrocarbon
• carbon black that may be used as a reinforcing agent may be the same as carbon black that was previously used in 1) the wet masterbatch.
• ultra-high-density carbon black having an iodine absorption amount of 200 to 1000 mg/g and an N-dibutyl phthalate (DBP) oil absorption amount of 150 to 800 ml/100 g may be preferable.
• DBP N-dibutyl phthalate
• the rubber composition for tire treads may include 50 to 200 parts by weight of the wet masterbatch, 60 to 70 parts by weight of the raw rubber, and 50 to 200 parts by weight of a carbon black.
• the content of the wet masterbatch is less than 50 parts by weight, improvement effects according to used of the wet masterbatch are insignificant.
• dispersion time due to heating during reaction should be decreased. Accordingly, dispersity may be decreased.
• grip performance may be deteriorated under a condition of heavy load, high slip and high speed.
• durability may be deteriorated.
• the rubber composition for tire treads may selectively, further include a variety of additives such as a vulcanizing agent, a vulcanization accelerator, a vulcanization acceleration aid, an aging preventing agent or an adhesive.
• the additives may be any one that is generally used in the art.
• the contents of additives are determined according to mixing ratios used in general rubber compositions for tire tread, and are not specifically limited.
• a sulfur-based vulcanizing agent is preferably used.
• the sulfur-based vulcanizing agent may use an inorganic vulcanizing agent such as sulfur powder (S), insoluble sulfur (S), precipitated sulfur (S), or colloidal sulfur.
• an inorganic vulcanizing agent such as sulfur powder (S), insoluble sulfur (S), precipitated sulfur (S), or colloidal sulfur.
• elemental sulfur, or a vulcanizing agent that produce sulfur e.g., an amine disulfide or polymeric sulfur, may be used.
• the vulcanizing agent is preferably included in an amount of 0.5 parts to 2 parts by weight with respect to 100 parts by weight of the raw rubber.
• the vulcanizing agent exhibits appropriate vulcanizing effects and the raw rubber is less sensitive to heat and is chemically stable.
• the vulcanization accelerator means an accelerator that accelerates the rate of vulcanization or facilities the retarding action in an initial vulcanization stage.
• the vulcanization accelerator may be any one selected form the group consisting of sulfenamide based compounds, thiazole based compounds, thiuram based compounds, thiourea based compounds, guanidine based compounds, dithiocarbamic acid based compounds, aldehyde amine based compounds, aldehyde ammonia based compounds, imidazoline-based compounds, xanthate based compounds and combinations thereof.
• CBS N-cyclohexyl-2-benzothiazole sulfenamide
• TBS N-tert-butyl-2-benzothiazole sulfenamide
• N,N-dicyclohexyl-2-benzothiazole sulfenamide N-oxydiethylene-2-benzothiazole sulfenamide
• MTT 2-mercaptobenzothiazole
• MBTS dibenzothiazole disulfide
• sodium salts of 2-mercaptobenzothiazole zinc salts of 2-mercaptobenzothiazole
• copper salts of 2-mercaptobenzothiazole copper salts of 2-mercaptobenzothiazole
• thiuram based vulcanization accelerator for example, any one thiuram based compound selected from the group consisting of tetramethylthiuram disulfide (TMTD), tetraethylthiuram disulfide, tetramethylthiuram monosulfide, dipentamethylenethiuram disulfide, dipentamethylenethiuram monosulfide, dipentamethylenethiuram tetrasulfide, dipentamethyelnethiuram hexasulfide, tetrabutylthiuram disulfide, pentamethylenethiuram tetrasulfide and combinations thereof may be used.
• TMTD tetramethylthiuram disulfide
• tetraethylthiuram disulfide tetramethylthiuram monosulfide
• dipentamethylenethiuram disulfide dipentamethylenethiuram monosulfide
• any one thiourea based compound selected from the group consisting of, for example, thiocarbamide, diethylthiourea, dibutylthiourea, trimethylthiourea, di-ortho-tolylthiourea and combinations thereof may be used.
• any one guanidine based compound selected from the group consisting of, for example, diphenylguanidine, di-ortho-tolylguanidine, triphenylguanidine, ortho-tolylbiguanide, diphenylguanidine phthalate and combinations thereof may be used.
• aldehyde amine based or aldehyde ammonia based vulcanization accelerator an aldehyde amine based compound or an aldehyde ammonia based compound selected from the group consisting of, for example, acetaldehyde-aniline reaction products, butyraldehydeaniline condensates, hexamethylenetetramine, acetaldehyde-ammonia reaction products and combinations thereof may be used.
• an imidazoline-based compound such as 2-mercaptoimidazoline
• a xanthate based compound such as zinc dibutyl xanthogenate
• the vulcanization accelerator may be included in an amount of 1.5 to 3.5 parts by weight with respect to 100 parts by weight of the raw rubber.
• the vulcanization acceleration aid is a mixing agent used in combination with the vulcanization accelerator in order to perfect the accelerating effect, and may be any one selected from the group consisting of inorganic vulcanization acceleration aids, organic vulcanization acceleration aids, and combinations thereof.
• any one selected from the group consisting of zinc oxide (ZnO), zinc carbonate, magnesium oxide (MgO), lead oxide, potassium hydroxide and combinations thereof may be used.
• organic vulcanization acceleration aid any one selected from the group consisting of stearic acid, zinc stearate, palmitic acid, linoleic acid, oleic acid, lauric acid, dibutyl ammonium oleate, derivatives thereof and combinations thereof may be used.
• zinc oxide and stearic acid may be used together as the vulcanization acceleration aid.
• zinc oxide is dissolved in stearic acid and forms an effective complex with the vulcanization accelerator, and thus, the complex produces free sulfur during the vulcanization reaction, thereby facilitating the crosslinking reaction of rubber.
• zinc oxide and stearic acid When zinc oxide and stearic acid are used together, zinc oxide and stearic acid may be respectively used in amounts of 1 to 5 parts by weight and 0.5 to 3 parts by weight, in order to function as an adequate vulcanization acceleration aid.
• vulcanization rate decreases and thus productivity may be deteriorated.
• scorching occurs and thus properties may be deteriorated.
• the aging preventing agent is an additive used to stop the chain reactions in which the tire is auto-oxidized by oxygen.
• the aging preventing agent any one selected from the group consisting of amines, phenols, quinolines, imidazoles, carbamic acid metal salts, waxes and combinations thereof may be appropriately selected and used
• any one selected from the group consisting of 2,2'-methylenebis(4-methyl-6-tert-butylphenol), 2,2'-isobutylidenebis(4,6-dimethylphenol), 2,6-di-t-butyl-p-cresol and combinations thereof may be used.
• 2,2,4-trimethyl-1,2-dihydroquinoline and derivatives thereof may be used, particularly, any one selected from the group consisting of 6-ethoxy-2,2,4-trimethyl-1,2-dihydroquinoline, 6-anilino-2,2,4-trimethyl-1,2-dihydroquinoline, 6-dodecyl-2,2,4-trimethyl-1,2-dihydroquinoline, and combinations thereof may be used.
• wax waxy hydrocarbons may be preferably used.
• the aging preventing agent when, in addition to the aging preventing action, conditions such as high solubility in rubber and low volatility, nonreactivity with rubber, and non-inhibition of vulcanization are considered, the aging preventing agent may be included in an amount of 1 parts to 6 parts by weight with respect to 100 parts by weight of the raw rubber.
• the adhesive contributes to enhancement of the properties of rubber by further enhancing adhesion between rubber and rubber, and improving compatibility, dispersibility and processability of other additives such as a filler.
• natural resin based adhesives such as rosin based resins and terpene based resins
• synthetic resin based adhesives such as petroleum resins, coal tar, and alkylphenol based resins
• rosin-based resins any one selected from the group consisting of rosin resin, a rosin ester resin, a hydrogenated rosin ester resin, derivatives thereof, and combinations thereof may be used.
• terpene based resins any one selected from the group consisting of a terpene resin, a terpene phenol resin, and combinations thereof may be used.
• any one selected from the group consisting of aliphatic resins, acid-modified aliphatic resins, alicyclic resins, hydrogenated alicyclic resins, aromatic (C9) resins, hydrogenated aromatic resins, C5-C9 copolymer resins, styrene resins, styrene copolymer resins, and combinations thereof may be used.
• the coal tar may be a coumarone-indene resin.
• p-tert-alkylphenol formaldehyde resins may be used, and the p-tert-alkylphenol formaldehyde resin may be any one selected from the group consisting of p-tert-butylphenol formaldehyde resin, p-tert-octylphenol formaldehyde, and combinations thereof.
• the adhesive may be included in an amount of 2 to 4 parts by weight with respect to 100 parts by weight of the raw rubber.
• content of the adhesive is less than 2 parts by weight with respect to 100 parts by weight of the raw rubber, adhesion performance may be deteriorated, and when the content of the adhesive exceeds 4 parts by weight, rubber properties may be deteriorated.
• the rubber composition for tire treads may be prepared through a general two-step process. That is, the rubber composition may be prepared in an appropriate mixer, using a first step of thermomechanically treating or kneading at high temperature of 110°C to 190°C, preferably at high temperature of 130°C to 180°C and a second step of mechanically treating typically at low temperature of less than 110°C, e.g., 40°C to 100°C during a finishing step in which a cross-linking system is mixed, but the present invention is not limited thereto.
• the rubber composition for tire treads may be included not only in the tread (tread cap and tread base), but also in various rubber constituent elements that constitute the tire.
• the rubber constituents include side walls, side wall inserts, apexes, chafers, wire coats, inner liners, etc.
• a tire according to another embodiment is manufactured using the rubber composition for tire treads.
• a method of manufacturing a tire using the rubber composition for tire treads may be any one of conventional manufacturing methods, and detailed description therefore is omitted.
• the tire examples include light truck radial (LTR) tires, ultra high performance (UHP) tires, tires for race cars, off-road tires, tires for airplanes, tires for agricultural machines, truck tires or bus tires.
• LTR light truck radial
• UHP ultra high performance
• the tire may be a radial tire or a bias tire, and the radial tire is preferable.
• a rubber composition for tire treads according to the present invention has enhanced grip and anti-wear performances under a condition of heavy load, high slip and high speed, and thus, may be usefully applied to an ultra-high performance tire.
• Rubber compositions for tire tread according to Examples and Comparative Examples were prepared using compositions summarized in Table 1 below. The rubber compositions were prepared according to a general rubber composition method. [Table 1] Comparative Example 1 Example 1 Example 2 Example 3 Example 4 Example 5 Example 6 Wet masterbatch 1) 190 190 190 190 190 190 Composition of wet masterbatch Styrene-butadiene latex 100 100 100 100 100 100 100 Carbon black 3) 140 140 140 140 140 140 140 140 140 140 140 140 140 140 Liquid SBR copolymer - 140 40 70 100 160 200 RAE oil 140 - 100 70 40 - - Raw material rubber 2) 60 60 60 60 60 60 60 Carbon black 3) 100 100 100 100 100 100 100 100 100 100 100 Petroleum based resin 4) 20 - - - - - - Aging preventing agent 6 6 6 6 6 6 6 Vulcanizing agent 0.8 0.8 0.8 0.8 0.8 0.8 0.8 Vulcanization accelerator 3 3 3 3 3 3 Unit: parts by weight 1) Wet masterbatch: 40 to 60
• Raw material rubber a styrene-butadiene rubber including 30 to 50 wt% of styrene, 40 to 65 wt% of vinyl in butadiene and 5 to 45 wt% of RAE oil and having Tg of -19 to -29°C was polymerized according to a batchwise method.
• Carbon black super-fine-particle-type carbon black having an iodine absorption amount of 200 to 1000 mg/g and a DBP oil absorption amount of 150 to 800 ml/100 g.
• Petroleum based resin petroleum based resin having a softening point of 50 to 90°C.
• treads were prepared using the rubber prepared according to Comparative Examples and Examples, and 240/640R18 F200 standard tires including the tread rubber as a semi-product were manufactured.
• the manufactured tires were subjected to measurement of anti-wear performance on a dry road, brake performance on a dry road, and a grip rate. Results are summarized in Table 3 below as relative ratios to the results of Comparative Example 1. [Table 3] Comparative Example 1 Example 1 Example 2 Example 3 Example 4 Example 5 Example 6 Anti-wear performance 100 100 101 101 100 101 100 101 100 101 100 Durability 100 100 101 101 100 101 100 101 100 Grip ratio 100 140 126 129 132 137 135

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• Chemical & Material Sciences (AREA)
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• Chemical Kinetics & Catalysis (AREA)
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• Polymers & Plastics (AREA)
• Organic Chemistry (AREA)
• Engineering & Computer Science (AREA)
• Mechanical Engineering (AREA)
• Compositions Of Macromolecular Compounds (AREA)
• Tires In General (AREA)
• Processes Of Treating Macromolecular Substances (AREA)

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• 2014
  • 2014-06-30 KR KR1020140080743A patent/KR101623027B1/ko active IP Right Grant
• 2015
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  • 2015-06-29 EP EP15174380.4A patent/EP2962870B1/en not_active Not-in-force
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